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HVAC SYSTEMS - HFT Stuttgart

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( T −T<br />

) ( T −T<br />

)<br />

col , m<br />

t<br />

amb<br />

col , m<br />

t<br />

Page - 17 -<br />

2<br />

amb<br />

CHAPTER 02<br />

η col = η0<br />

− a1<br />

− a2<br />

(2.2.1-3)<br />

G<br />

G<br />

If the collector mean temperature Tcol,m is approximated by the mean<br />

temperature of the collector inlet Tcol,in and collector outlet Tcol,out<br />

Tcol<br />

, in + Tcol<br />

, out<br />

Tcol<br />

, m = ,<br />

2<br />

(2.2.1-4)<br />

the useful heating power of the collector is given by<br />

( T −T<br />

)<br />

& η &<br />

(2.2.1-5)<br />

Q col = col ⋅G<br />

t ⋅ A = mfluidc<br />

fluid ⋅ col , out col , in<br />

The solution of equation 2.2.1-3 and 2.2.1-5 for the collector outlet temperature<br />

leads to a quadratic equation with the solutions<br />

Tcol , out 1/<br />

2<br />

p<br />

= − ±<br />

2<br />

and the coefficients:<br />

2<br />

⎛ p ⎞<br />

⎜ ⎟<br />

⎝ 2 ⎠<br />

− q<br />

2a1<br />

2m&<br />

fluid ⋅ c fluid<br />

p = + 2T<br />

col , in − 4T<br />

a +<br />

a2<br />

A ⋅ a2<br />

⎛ 2a1<br />

2m&<br />

fluid ⋅ c<br />

q = ⎜ − 4T<br />

a + Tcol<br />

, in −<br />

⎝ a2<br />

A ⋅ a2<br />

⎛G<br />

tη0<br />

a1Ta<br />

2 ⎞<br />

−4<br />

⋅ ⎜ + + T ⎟ a<br />

⎝ a2<br />

a2<br />

⎠<br />

fluid<br />

⎞<br />

⎟ ⋅T<br />

⎠<br />

col , in<br />

(2.2.1-6)<br />

(2.2.1-7)<br />

(2.2.1-8)<br />

This simple model requires only the efficiency parameters of the collector zero<br />

efficiency η0, linear heat loss coefficient a1, and quadratic heat loss coefficient<br />

a2 together with the reference gross aperture or absorber area. These values<br />

are provided on the product datasheet of the collectors. This block was already<br />

available and is called ‘SCETA’ and can be found in the thermal tool box of<br />

INSEL.

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